Mixture of Ethyl Acetate + Ethane, 1,2-dichloro-

Datasets

1. Mole fraction
2. Excess molar enthalpy (molar enthalpy
3. P_vap - Vapor or sublimation pressure, kPa
4. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Ethane, 1,2-dichloro- (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Mole fraction of Ethane, 1,2-dichloro- (2) - Gas
0.1523	0.1146
0.2147	0.1648
0.2835	0.2216
0.3225	0.2663
0.4036	0.3462
0.4253	0.3727
0.5301	0.4900
0.5472	0.5108
0.5831	0.5541
0.6198	0.5958
0.6402	0.6182
0.6789	0.6640
0.7503	0.7445
0.7825	0.7796
0.8282	0.8319
0.8964	0.9005
0.9393	0.9445
0.9782	0.9814

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0368	-0.0393
0.0819	-0.0877
0.1310	-0.1442
0.1846	-0.2054
0.2408	-0.2686
0.2950	-0.3261
0.3419	-0.3628
0.3836	-0.3911
0.4244	-0.4217
0.4600	-0.4427
0.4728	-0.4459
0.4972	-0.4506
0.5087	-0.4509
0.5523	-0.4494
0.6040	-0.4362
0.6668	-0.4036
0.7470	-0.3375
0.8328	-0.2427
0.9184	-0.1347

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1523	24.14
0.2147	23.67
0.2835	23.04
0.3225	22.66
0.4036	22.03
0.4253	21.86
0.5301	21.37
0.5472	21.28
0.5831	21.14
0.6198	21.07
0.6402	21.02
0.6789	20.94
0.7503	20.82
0.7825	20.77
0.8282	20.73
0.8964	20.71
0.9393	20.76
0.9782	20.81

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.325 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Ethyl Acetate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0497	1223.67
0.0983	1202.79
0.1492	1181.45
0.1997	1160.95
0.2524	1140.18
0.3059	1119.62
0.3618	1098.71
0.4184	1078.16
0.4765	1057.68
0.5356	1037.35
0.5982	1016.38
0.6603	996.21
0.7247	975.88
0.7893	955.96
0.8570	935.65
0.9280	914.85

Mass density, kg/m3 [ref]

Fixed			Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Mass density, kg/m3 - Liquid
101.33	288.15	0.0000	906.71
101.33	288.15	0.1036	936.39
101.33	288.15	0.2054	966.98
101.33	288.15	0.3019	996.99
101.33	288.15	0.4003	1028.99
101.33	288.15	0.4963	1061.48
101.33	288.15	0.6020	1098.83
101.33	288.15	0.6820	1128.5
101.33	288.15	0.8002	1174.96
101.33	288.15	0.9001	1216.19
101.33	288.15	1.0000	1260.13
101.33	298.15	0.0000	894.97
101.33	298.15	0.1036	924.54
101.33	298.15	0.2054	954.82
101.33	298.15	0.3019	984.84
101.33	298.15	0.4003	1016.64
101.33	298.15	0.4963	1048.95
101.33	298.15	0.6020	1086.09
101.33	298.15	0.6820	1115.64
101.33	298.15	0.8002	1161.78
101.33	298.15	0.9001	1202.79
101.33	298.15	1.0000	1246.59
101.33	308.15	0.0000	882.27
101.33	308.15	0.1036	911.53
101.33	308.15	0.2054	941.7
101.33	308.15	0.3019	971.32
101.33	308.15	0.4003	1002.93
101.33	308.15	0.4963	1035.07
101.33	308.15	0.6020	1071.98
101.33	308.15	0.6820	1101.3
101.33	308.15	0.8002	1147.08
101.33	308.15	0.9001	1187.86
101.33	308.15	1.0000	1231.27
200.00	298.15	0.2995	983.88
200.00	298.15	0.5013	1046.97
200.00	298.15	0.6994	1120.18
500.00	298.15	0.2995	984.27
600.00	298.15	0.5013	1047.36
600.00	298.15	0.6994	1120.72
1100.00	298.15	0.5013	1047.97
1200.00	298.15	0.2995	985.01
1200.00	298.15	0.6994	1121.21
2100.00	298.15	0.5013	1049.05
2100.00	298.15	0.6994	1122.19
2300.00	298.15	0.2995	986.02
2900.00	298.15	0.2995	986.78
3000.00	298.15	0.6994	1122.99
3200.00	298.15	0.5013	1050.04
3900.00	298.15	0.5013	1050.82
4000.00	298.15	0.2995	987.78
4000.00	298.15	0.6994	1124.04
4800.00	298.15	0.5013	1051.57
4800.00	298.15	0.6994	1124.91
5000.00	298.15	0.2995	988.82
5900.00	298.15	0.2995	989.64
6100.00	298.15	0.5013	1052.93
6100.00	298.15	0.6994	1126.11
6900.00	298.15	0.2995	990.62
7000.00	298.15	0.6994	1126.84
7100.00	298.15	0.5013	1053.82
7800.00	298.15	0.2995	991.51
7800.00	298.15	0.5013	1054.57
8000.00	298.15	0.6994	1127.94
8600.00	298.15	0.2995	992.31
8800.00	298.15	0.6994	1128.76
9000.00	298.15	0.5013	1055.76
9800.00	298.15	0.5013	1056.47
9900.00	298.15	0.2995	993.71
9900.00	298.15	0.6994	1129.84
11700.00	298.15	0.2995	995.34
11900.00	298.15	0.5013	1058.45
12000.00	298.15	0.6994	1131.77
13700.00	298.15	0.6994	1133.5
13800.00	298.15	0.2995	997.35
13800.00	298.15	0.5013	1060.29
15600.00	298.15	0.6994	1135.23
15900.00	298.15	0.2995	999.26
15900.00	298.15	0.5013	1062.3
17700.00	298.15	0.6994	1137.32
17900.00	298.15	0.2995	1001.14
18000.00	298.15	0.5013	1064.25
19400.00	298.15	0.2995	1002.51
19600.00	298.15	0.6994	1139.1
19900.00	298.15	0.5013	1065.99

Sources

• Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 K

Note: These property values are available through the Cheméo API. A free account gives you an access key.